US20120028117A1 - Fluorinated binder composite materials and carbon nanotubes for positive electrodes for lithium batteries - Google Patents

Fluorinated binder composite materials and carbon nanotubes for positive electrodes for lithium batteries Download PDF

Info

Publication number
US20120028117A1
US20120028117A1 US13/256,522 US201013256522A US2012028117A1 US 20120028117 A1 US20120028117 A1 US 20120028117A1 US 201013256522 A US201013256522 A US 201013256522A US 2012028117 A1 US2012028117 A1 US 2012028117A1
Authority
US
United States
Prior art keywords
composite material
suspension
electrode
weight
pvdf
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Abandoned
Application number
US13/256,522
Other languages
English (en)
Inventor
Dominique Plee
Bernard Lestriez
Sabrina Desaever
Dominique Guyomard
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Centre National de la Recherche Scientifique CNRS
Arkema France SA
Original Assignee
Centre National de la Recherche Scientifique CNRS
Arkema France SA
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Centre National de la Recherche Scientifique CNRS, Arkema France SA filed Critical Centre National de la Recherche Scientifique CNRS
Assigned to ARKEMA FRANCE, CENTRE NATIONAL DE LA RECHERCHE SCIENTIFIQUE reassignment ARKEMA FRANCE ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: PLEE, DOMINIQUE, LESTRIEZ, BERNARD, GUYOMARD, DOMINIQUE, DESAEVER, SABRINA
Publication of US20120028117A1 publication Critical patent/US20120028117A1/en
Abandoned legal-status Critical Current

Links

Images

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/624Electric conductive fillers
    • H01M4/625Carbon or graphite
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B82NANOTECHNOLOGY
    • B82YSPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
    • B82Y30/00Nanotechnology for materials or surface science, e.g. nanocomposites
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/131Electrodes based on mixed oxides or hydroxides, or on mixtures of oxides or hydroxides, e.g. LiCoOx
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/139Processes of manufacture
    • H01M4/1391Processes of manufacture of electrodes based on mixed oxides or hydroxides, or on mixtures of oxides or hydroxides, e.g. LiCoOx
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/621Binders
    • H01M4/622Binders being polymers
    • H01M4/623Binders being polymers fluorinated polymers
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • H01M10/0525Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/04Processes of manufacture in general
    • H01M4/043Processes of manufacture in general involving compressing or compaction
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Definitions

  • the invention relates generally to the field of the storage of electrical energy in secondary lithium batteries of Li-ion type. More specifically, the invention relates to a material for the positive electrode of an Li-ion battery, to its method of preparation and to its use in an Li-ion battery. Another subject matter of the invention is the Li-ion batteries manufactured by incorporating this composite electrode material.
  • the electrode material according to the invention can be used in a secondary Li-ion battery comprising a nonaqueous electrolyte, on which it confers excellent characteristics of capacity and cycling under high current density.
  • An Li-ion battery comprises at least one negative electrode or anode coupled to a current collector made of copper, a positive electrode or cathode coupled to a current collector made of aluminum, a separator and an electrolyte.
  • the electrolyte is composed of a lithium salt, generally lithium hexafluorophosphate, mixed with a solvent which is a mixture of organic carbonates which are chosen in order to optimize the transportation and the dissociation of the ions.
  • a high dielectric constant promotes the dissociation of the ions and thus the number of ions available in a given volume, whereas a low viscosity promotes ion diffusion, which plays an essential role, among other parameters, in the charge and discharge rates of the electrochemical system.
  • An electrode generally comprises at least one current collector on which is deposited a composite material which is composed of: an “active” material, as it exhibits an electrochemical activity with regard to lithium, a polymer, which acts as binder and which is generally a vinylidene fluoride copolymer for the positive electrode and aqueous-based binders, of carboxymethylcellulose type, or styrene-butadiene latexes for the negative electrode, plus an additive which conducts electrons, which is generally carbon black Super P or acetylene black.
  • lithium is inserted into the active material of the negative electrode (anode) and its concentration is kept constant in the solvent by the extraction of an equivalent amount of the active material of the positive electrode (cathode).
  • the insertion into the negative electrode is reflected by a reduction of the lithium and it is therefore necessary to contribute, via an external circuit, the electrons to this electrode originating from the positive electrode.
  • the reverse reactions take place.
  • the conventional active materials are graphite at the negative electrode and cobalt oxide at the positive electrode.
  • Li-ion batteries are used today above all in the fields of mobile phones, computers and lightweight equipment but a few niche markets exist, such as the space industry, aeronautical industry and defense applications.
  • electrochemical storage appears a method of choice in making possible optimum use and optimum management of the production of energy by the intermittent renewable energy sources which are solar power and wind power.
  • Li-ion batteries exhibit virtually the highest energy density among rechargeable systems and are thus widely envisaged as source of electrical energy in electric vehicles and hybrid vehicles in the future, in particular those which would make it possible to directly recharge via the mains.
  • Li-ion batteries retain some disadvantages, related in particular to safety (possibility of decomposition of the electrolyte and of the solvent with release of gas, risk of explosion and/or of ignition) and to the still high cost of the kWh stored, which has led to numerous studies on alternative active materials, both with the positive electrode (phosphates, various oxides, and the like) and with the negative electrode (silicon, tin, various alloys, and the like).
  • Cobalt oxide exhibits an advantageous voltage difference with respect to lithium, a good capacity and a very reasonable aging quality but runaway reactions can occur and be reflected by overheating, decomposition of solvent and electrolytes, indeed even explosions and fires, if the internal pressure exceeds the resistance of the casing of the battery. This characteristic renders the motor vehicle application out of the question. Furthermore, cobalt is now included among expensive materials and those of limited availability.
  • iron phosphate has a good capacity by weight of the order of 160 mAh/g, scarcely inferior to that of cobalt oxide, but, in terms of performance by volume, the difference is accentuated because the density of iron phosphate is only 3.5.
  • a second disadvantage is its low electrical conductivity and it is for this reason that it is supplied covered with a carbon-based coating.
  • CNTs carbon nanotubes
  • CNT in composite materials for a positive electrode is furthermore described in various documents, in particular in the patent applications US 2008/038635, JP 2003-331838, JP 2003-092105 or JP 07-014582.
  • the document CN 101 192 682 describes a secondary Li-ion battery comprising an anode composed of a mixture of a complex lithium oxide, such as a mixed Ni—Co—Li, Mn—Li or Mn—B—Li oxide, with carbon nanotubes as conductive agents in a portion of 0.1 to 3% by weight and a polymer binder, such as PVDF or PTFE.
  • a complex lithium oxide such as a mixed Ni—Co—Li, Mn—Li or Mn—B—Li oxide
  • carbon nanotubes as conductive agents in a portion of 0.1 to 3% by weight
  • a polymer binder such as PVDF or PTFE.
  • the document EP 2 034 541 describes a process for the preparation of composite materials for a positive electrode of a lithium battery comprising lithium manganate, CNTs, carbon black and a fluoropolymer binder.
  • the electrode active substance for a secondary lithium battery is preferably chosen from transition metal oxides, such as lithium cobalt oxide LiCoO 2 , lithium nickel oxide LiNiO 2 , lithium manganese oxide (LiMn 2 O 4 ) or mixed oxides based on several transition metals.
  • the invention relates to a composite material for a positive electrode of an Li-ion battery, comprising:
  • the compounds having polyanionic frameworks are mixed phosphates or silicates of lithium and of a metal atom M. More particularly, they are mixed phosphates.
  • the compounds having polyanionic frameworks have a structure of masicon or olivine type.
  • M is chosen from Fe, Mn or their combination.
  • the lithium insertion compound is LiFePO 4 .
  • the CNTs forming part of the structure of the composite material according to the invention have a fibrillar morphology. They generally have diameters of 10 to 50 nm, preferably of 10 to 20 nm, on average.
  • the length of the carbon nanotubes is generally of the order of 5-15 ⁇ m but some dispersing processes may reduce it, in particular ultrasound.
  • This conductive additive differs from the usual conductive additives, such as SP carbon, acetylene black or graphite, in a very high aspect ratio. The latter is defined as the ratio of the greatest dimension to the smallest dimension of the particles. This ratio is of the order of 30 to 1000 for CNTs, as opposed to 3 to 10 for SP carbon, acetylene black and graphite.
  • the CNTs play, in the electrode composite material, an important role with regard to maintaining the capacity as a function of the current density, maintaining the capacity in cycling, which allows excellent cycling stability, this being the case at high contents of active material (for example up to 94%) in the composite electrode material.
  • the carbon nanotubes forming part of the structure of the composite material according to the invention have a content of transition metals of less than 1000 ppm by weight, measured by conventional chemical analysis, and preferably of less than 500 ppm. Excessively high contents of transition metals are believed to reduce the lifetime of the batteries, in particular at high temperature, and to increase the operating risks. However, to produce such nanotubes can prove to be expensive and can result in excessive battery manufacturing costs. The Applicant Company has found, surprisingly, that some nanotubes comprising markedly greater proportions than those mentioned above do not present problems in practice.
  • crude carbon nanotubes comprising residues of synthesis catalyst have proved to be entirely usable in the composite material according to the invention; they exhibit an electrochemical signature in cyclic voltammetry such that a persistence and a complete reversibility of the oxidation/reduction phenomena are observed.
  • conductive additives can be added to the composite material: graphite, carbon black, such as acetylene black, SP carbon or carbon nanofibers.
  • commercial conductive additives meet this condition. Mention may in particular be made of the compounds Ensagri Super S® or Super P®, sold by Chemetals, or the VGCF nanofibers, sold by Showa Denko.
  • the polymer binder can be chosen from: polysaccharides, modified polysaccharides, latexes, polyelectrolytes, polyethers, polyesters, polyacrylic polymers, polycarbonates, polyimines, polyamides, polyacrylamides, polyurethanes, polyepoxides, polyphosphazenes, polysulfones, or halogenated polymers.
  • halogenated polymer of homopolymers and copolymers of vinyl chloride, of vinylidene fluoride, of vinylidene chloride, of tetrafluoroethylene or of chlorotrifluoroethylene, and copolymers of vinylidene fluoride and of hexafluoropropylene (PVDF-HFP).
  • the term “copolymer” is understood to mean, in the present text, a polymer compound obtained from at least two different monomers. Blends of polymers are also advantageous. Mention may be made of the blends of carboxymethylcellulose with styrene/butadiene, acrylic and nitrile rubber latexes. Water-soluble polymers are particularly preferred. In particular, aqueous latexes of fluorocopolymers or fluorohomopolymers are particularly preferred.
  • the polymer binder is chosen from the group: PVDF, PVDF/HFP or PVDF/PCTFE copolymers, blends of PVDF and of a PVDF comprising polar functional groups, and fluoroterpolymers.
  • the invention relates to a process for the preparation of an electrode composite material which comprises the following operations:
  • the polymer is introduced in the pure state or in the form of a solution in a volatile solvent; the CNTs are introduced in the pure state or in the form of a suspension in a volatile solvent.
  • the CNTs are those sold under the Graphistrength® C100 name by Arkema, exhibiting the following characteristics: the CNTs are multiwall nanotubes having from 5 to 15 walls, a mean external diameter ranging from 10 to 15 nm and a length ranging from 0.1 to 10 ⁇ m.
  • the carbon nanotubes are difficult to disperse. Nevertheless, by virtue of the process according to the invention, it is possible to distribute them in the electrode composite material in such a way that they form a meshwork around the particles of active material and thus play a role both of conductive additive and also of mechanical maintenance, which is important in order to accommodate the variations in volume during the charging/discharging stages. On the one hand, they provide for the delivery of the electrons to the active material particles and, on the other hand, due to their length and their flexibility, they form electrical bridges between the active material particles which move about as a result of their variation in volume.
  • the volatile solvent is an organic solvent or water or a mixture of organic solvent and of water. Mention may be made, among organic solvents, of N-methylpyrrolidone (NMP) or dimethyl sulfoxide (DMSO) or dimethylformamide (DMF).
  • NMP N-methylpyrrolidone
  • DMSO dimethyl sulfoxide
  • DMF dimethylformamide
  • the suspension can be prepared in a single stage or in two or three successive stages.
  • one embodiment consists of the mixing of all the constituents, followed by the mechanical dispersing stage.
  • one embodiment consists in preparing a first dispersion, comprising the solvent, the CNTs and optionally all or part of the polymer binder, using mechanical means, and in then adding, to this first dispersion, the other constituents of the composite material, this new suspension being used for the preparation of the final film.
  • one embodiment consists in preparing a dispersion comprising the CNTs and optionally all or part of the polymer binder in a solvent, in then adding the active material, in removing the solvent in order to obtain a powder and in then forming a new suspension by adding solvent and the remainder of the constituents of the composite material to this powder, this new suspension being used for the preparation of the final film.
  • a preferred method for forming and homogenizing the dispersion consists in preparing a suspension of solvent, of polymer and of CNT which is subjected to the mechanical dispersing process, before the addition of the active material.
  • Another preferred method for forming and homogenizing the dispersion consists in preparing a suspension of solvent and of CNT which is subjected to said mechanical dispersing process, before the addition of the binders and active material.
  • the level of performance achieved for the Li-ion battery incorporating the composite material of a positive electrode obtained according to the process of the invention results from the conditions of preparation of said material, in particular the stage of predispersing the CNTs by milling, and the quality of the dispersing, which is preferably carried out over a long period of time, generally of greater than 10 hours, which is not obvious to a person skilled in the art.
  • the quality of the dispersing is assessed on the basis of the values of the storage modulus G′, which is obtained by frequency rheological measurements, which measurements give access to two parameters G′ and G′′, respectively storage modulus and loss modulus.
  • the CNT suspension prepared according to the invention exhibits, for a frequency of 1 Hz, a storage modulus G′ as follows:
  • the film can be obtained from the suspension by any conventional means, for example by extrusion, by tape casting or by spray drying on a substrate, followed by drying.
  • a metal sheet capable of acting as collector for the electrode for example an aluminum sheet or grid treated with a corrosion-resistant coating.
  • the film on a substrate thus obtained can be used directly as electrode.
  • This film can optionally be made denser by application of a pressure (between 0.1 and 10 tonnes/cm 2 ).
  • the composite material according to the invention is of use in the preparation of electrodes for electrochemical devices, in particular in lithium batteries.
  • Another subject-matter of the invention is composed of a positive electrode of an Li-ion battery comprising at least one current collector on which is deposited a composite material according to the invention or obtained according to the process of the invention.
  • Another subject matter of the invention consists of an Li-ion battery incorporating said positive electrode.
  • a lithium battery comprises a negative electrode, composed of lithium metal, a lithium alloy or a lithium insertion compound, and a positive electrode, the two electrodes being separated by a solution of a salt, the cation of which comprises at least one lithium ion, such as, for example, LiPF 6 , LiAsF 6 , LiClO 4 , LiBF 4 , LiC 4 BO 8 , Li(C 2 F 5 SO 2 ) 2 N, Li[(C 2 F 5 ) 3 PF 3 ], LiCF 3 SO 3 , LiCH 3 SO 3 , LiN(SO 2 CF 3 ) 2 , LiN(SO 2 F) 2 , and the like, in an aprotic solvent (ethylene carbonate, propylene carbonate, dimethyl carbonate, diethyl carbonate, methyl carbonate, and the like), the combined mixture acting as electrolyte.
  • aprotic solvent ethylene carbonate, propylene carbonate, dimethyl carbonate, diethyl carbonate, methyl carbonate, and the
  • the positive electrode is composed of the composite material, the active substance of which represents from 80% to 97%.
  • the content of polymeric binder is between 0.1 and 10% and the content of carbon nanotubes is between 1% and 2.5% by weight, preferably between 1.5% and 2.2% by weight, of the weight of the dry electrode.
  • the invention also relates to the use of a composite material comprising:
  • the invention also relates to the use of a composite material obtained according to the process described above in the manufacture of Li-ion batteries.
  • the composite material is composed of 94% by weight of C/LiFePO 4 with a carbon coating, the latter representing 1-3% of the total weight of C/LiFePO 4 , of 4% by weight of the PVDF binder supplied by Arkema under the Kynar® brand, 1 ⁇ 3 of which is composed of Kynar® ADX and 2 ⁇ 3 of which is composed of Kynar® HSV 900, and of 2% by weight of CNTs supplied by Arkema under the name Graphistrength® C100.
  • These nanotubes have a mean diameter of 20 nm and a length estimated at a few microns and their chemical composition shows that they comprise approximately 7% of inorganic ash resulting from the synthesis process.
  • the mixture is comilled in a jar made of chromium stainless steel with a volume of 250 ml, containing a mixture of beads made of chromium stainless steel with a diameter of 10 and 5 mm, by a planetary mill for 24 h. After drying at 120° C., the mixture is treated at 600° C. for 6 h in an atmosphere of argon (with 2% of H 2 ).
  • a first stage all of the CNTs participating in the composition of the composite material are first of all dispersed in NMP using a bead mill (Pulverisette 7, Fritsch).
  • the conditions of the dispersing are 700 revolutions/minute and a 12.5 ml milling chamber containing three beads with a diameter of 10 mm, 0.360 ml of NMP and 8 mg of CNT.
  • the duration of the dispersing varies from 6 to 48 h.
  • the C/LiFePO 4 particles (376 mg), 16 mg of PVDF and 0.640 ml of NMP are added to the dispersion of the CNTs and everything is mixed by comilling at 700 revolutions/minute for 1 h 30.
  • the composite material constitutes 29% by weight of the suspension, the remainder being NMP.
  • the electrode is prepared by coating the suspension comprising the composite onto a current collector made of aluminum with a thickness of 25 ⁇ m.
  • the height of the scraper of the coating machine is set at 180 ⁇ m.
  • the electrode is dried overnight in an oven at 70° C. It is then made dense under 62.5 MPa. It is subsequently again dried in an oven at 70° C. overnight and finally at 100° C. under vacuum for 1 h. After drying, the amount of electrode deposited per unit of surface area of current collector is measured: 4 mg/cm 2 .
  • the electrode thus obtained was fitted to a battery having, as negative electrode, a sheet of lithium metal rolled onto a current collector made of nickel, a separator made of fiber glass and a liquid electrolyte composed of a 1M solution of LiPF 6 dissolved in a 1:1 mixture of ethylene carbonate and dimethyl carbonate (EC/DMC).
  • EC/DMC ethylene carbonate and dimethyl carbonate
  • the evaluation of the electrochemical performance was carried out in the potential range 2-4.3 V vs. Li + /Li, in galvanostatic mode.
  • a current I of 1 A/g corresponds to a 6C rate (duration of charging or discharging 10 minutes).
  • FIG. 1 represents the change in the capacity Q (in mAh/g) at a 6C rate (1 A/g) as a function of the duration of the dispersing of the CNTs. The best electrochemical performance is obtained for an optimum dispersing time of 15 h.
  • FIG. 2 gives the rheological characteristics of the CNT dispersion after milling for 15 h.
  • a solids content of CNT 8 mg in 0.360 ml of NMP, an optimum electrochemical performance is obtained when the storage module G′ reaches a value of at least 250 Pa in the frequency range 0.1 to 100 Hz.
  • composition of the composite material of this example is identical to that of example 1.
  • the preparation differs from that given in example 1 in that the PVDF binder is introduced, in the powder form, during the first stage, that is to say during the dispersing of the CNTs.
  • all of the CNTs and of the PVDFs participating in the composition of the composite material are first of all dispersed in NMP using a bead mill (Pulverisette 7, Fritsch).
  • the conditions of the dispersing are 700 revolutions/minute and a 12.5 ml milling chamber containing three beads with a diameter of 10 mm, 0.360 ml of NMP, 8 mg of CNT and 16 mg of PVDF.
  • the duration of the dispersing varies from 6 to 48 h.
  • the C/LiFePO 4 particles (376 mg) and 0.640 ml of NMP are added and everything is mixed by comilling at 700 revolutions per minute for 1 h 30.
  • the composite material constitutes 29% by weight of the suspension, the remainder being NMP.
  • the electrode and the battery are subsequently prepared and the electrochemical performance is evaluated as in example 1.
  • FIG. 3 represents the change in the capacity Q (in mAh/g) at a 6C rate as a function of the duration of the dispersing of the CNT+PVDF mixture. The best electrochemical performance is obtained for an optimum dispersing time of 24 h.
  • composition of the composite material of this example is identical to that of example 1.
  • the preparation differs from that given in example 1 in the following characteristics: during the first stage, the duration of the dispersing of the CNTs is 15 h; during the second stage, the composite material constitutes 32% by weight of the suspension; and, during the third stage, the height of the scraper is set at 300 ⁇ m and the densifying pressure is 750 MPa. After the third stage, the amount of electrode deposited per unit of surface area of current collector is measured: 7 mg/cm 2 .
  • the electrode (a) thus obtained was fitted to a battery having, as negative electrode, a sheet of lithium metal rolled onto a current collector made of nickel, a separator made of fiber glass and a liquid electrolyte composed of a 1M solution of LiPF 6 dissolved in 1:1 EC/DMC.
  • the electrochemical performance was measured and compared with those of similar batteries in which the positive electrode is an electrode having the following initial composition:
  • the amount of electrode deposited per unit of surface area of current collector is 7 mg/cm 2 for (b) and (c).
  • FIG. 4 represents the change in the capacity Q (in mAh/g) as a function of the current by weight.
  • the correspondence between the two curves and the samples is as follows:
  • Curve - ⁇ -- ⁇ - sample a according to the invention
  • Curve - ⁇ -- ⁇ - comparative sample b
  • Curve - ⁇ -- ⁇ - comparative sample c
  • the comparison of the curves shows better maintenance of the capacity as a function of the current density for the electrode according to the invention.
  • the capacity restored at a 6C rate is 120 mAh/g of C/LiFePO 4 with the CNTs, 100 mAh/g with the acetylene black and 85 mAh/g with the VGCFs.
  • the restored capacity is related to the weight of electrode, the following results are obtained: 113 mAh/g of electrode with the CNTs, 91 mAh/g with acetylene black and 78 mAh/g with the VGCFs, which demonstrate the superiority of the electrode (a) according to the invention.
  • composition of the composite material of this example is 94.3% of C/LiFePO 4 , 1.7% of CNT and 4% of PVDF.
  • the material was prepared in the same way as the material of example 3.
  • the electrode (a) thus obtained was fitted to a battery having, as negative electrode, a sheet of lithium metal rolled onto a current collector made of nickel, a separator made of fiber glass and a liquid electrolyte composed of a 1M solution of LiPF 6 dissolved in 1:1 EC/DMC.
  • the electrochemical performance was measured and compared with those of similar batteries in which the positive electrode is an electrode having the following initial composition:
  • FIG. 5 represents the change in the capacity Q (in mAh/g) as a function of the cycle number for the three samples (a), (b) and (c).
  • the charge current by weight corresponds to a C rate and the discharge current by weight corresponds to a 2C rate.
  • Curve - ⁇ -- ⁇ - sample a according to the invention
  • Curve - ⁇ -- ⁇ - comparative sample b
  • Curve - ⁇ -- ⁇ - comparative sample c
  • composition of the composite material of this example is 94.3% of C/LiFePO 4 , 1.7% of CNT and 4% of PVDF.
  • the material was prepared in the same way as the material of example 4, except for one difference, namely that the CNTs were purified so as to reduce the iron content. After treatment, this content was found to be 215 ppm.
  • the electrode (a′) thus obtained was fitted to a battery having, as negative electrode, a sheet of lithium metal rolled onto a current collector made of nickel, a separator made of fiber glass and a liquid electrolyte composed of a 1M solution of LiPF 6 dissolved in 1:1 EC/DMC.
  • the electrochemical performance was measured and compared with those of similar batteries in which the positive electrode is an electrode having the following initial composition:
  • Table 1 below shows the comparison in performances for the four systems, in initial and final capacities.
  • composition of the composite material of this example is similar to that of examples 1 to 3, 94% of C/LiFePO 4 , 2% of CNT and 4% of PVDF. It is prepared as follows: all of the CNTs participating in the composition of the composite material are first of all dispersed in NMP. On conclusion of the dispersing, C/LiFePO 4 particles and NMP are added and everything is mixed by comilling. The NMP is subsequently removed by drying and the powder obtained is recovered. It is subsequently dispersed in a solution of PVDF in NMP.
  • a first stage all of the CNTs participating in the composition of the composite material are first of all dispersed in NMP using a bead mill (Pulverisette 7, Fritsch).
  • the conditions of the dispersing are 700 revolutions/minute for 15 hours and a 12.5 ml milling chamber containing three beads with a diameter of 10 mm, 0.360 ml of NMP and 9.6 mg of CNT.
  • the C/LiFePO 4 particles (447.4 mg) and 0.640 ml of NMP are added to the dispersion of the CNTs and everything is mixed by comilling at 700 revolutions per minute for 1 h 30.
  • the suspension is dried in an oven at 70° C. overnight, on conclusion of which a powder is recovered composed of 2.1% by weight of CNT and 97.9% by weight of C/LiFePO 4 .
  • this powder and 19 mg of PVDF are dispersed in 1 ml of NMP by comilling at 700 revolutions per minute for 1 h 30.
  • the composite material constitutes 32% by weight of the suspension, the remainder being NMP.
  • the electrode is prepared by coating the suspension comprising the composite onto a current collector made of aluminum with a thickness of 25 ⁇ m.
  • the height of the scraper of the coating machine is set at 300 ⁇ m.
  • the electrode is dried in an oven at 70° C. overnight. It is then made dense under 750 MPa. It is subsequently again dried in an oven at 70° C. overnight and finally at 100° C. under vacuum for 1 h. After drying, the amount of electrode deposited per unit of surface area of current collector is measured: 9 mg/cm 2 .
  • the electrode thus obtained was fitted to a battery having, as negative electrode, a sheet of lithium metal rolled onto a current collector made of nickel, a separator made of glass fiber and a liquid electrolyte composed of a 1M solution of LiPF 6 dissolved in 1:1 EC/DMC.
  • FIG. 6 represents the change in the capacity Q (in mAh/g) as a function of the cycle number at a C/5 rate and, in discharge, at a D/2.5 rate.
  • FIG. 7 represents the change in the capacity Q (in mAh/g) as a function of the current by weight. It is observed that the composite material according to the invention exhibits a good electrochemical performance.
  • Curve - ⁇ - sample according to the invention of example 6
  • Curve - ⁇ - sample according to the invention of example 7
  • composition of the composite material of this example is 94% C/LiFePO 4 , 2% CNT and 4% of a mixture of carboxymethylcellulose (CMC) and styrene/butadiene (SBR).
  • CMC carboxymethylcellulose
  • SBR styrene/butadiene
  • a first stage all of the CNTs participating in the composition of the composite material are first of all dispersed in NMP using a bead mill (Pulverisette 7, Fritsch).
  • the conditions of the dispersing are 700 revolutions/minute for 15 hours and a 12.5 ml milling chamber containing three beads with a diameter of 10 mm, 0.360 ml of NMP and 9.6 mg of CNT.
  • the C/LiFePO 4 particles (447.4 mg) and 0.640 ml of NMP are added to the dispersion of the CNTs and everything is mixed by comilling at 700 revolutions per minute for 1 h 30.
  • the suspension is dried in an oven at 70° C. overnight, on conclusion of which a powder is recovered composed of 2.1% by weight of CNT and 97.9% by weight of C/LiFePO 4 .
  • this powder and 19 mg of CMC+SBR are dispersed in 1 ml of deionized water by comilling at 700 revolutions per minute for 1 h 30.
  • the composite material constitutes 32% by weight of the suspension, the remainder being deionized water.
  • the electrode is prepared by coating the suspension comprising the composite onto a current collector made of aluminum with a thickness of 25 ⁇ m.
  • the height of the scraper of the coating machine is set at 300 ⁇ m.
  • the electrode is dried at ambient temperature overnight. It is then made dense under 750 MPa. It is subsequently dried at 100° C. under vacuum for 1 h. After drying, the amount of electrode deposited per unit of surface area of current collector is measured: 6 mg/cm 2 .
  • the electrode thus obtained was fitted to a battery having, as negative electrode, a sheet of lithium metal rolled onto a current collector made of nickel, a separator made of glass fiber and a liquid electrolyte composed of a 1M solution of LiPF 6 dissolved in 1:1 EC/DMC.
  • FIG. 6 represents the change in the capacity Q (in mAh/g) as a function of the cycle number at a C/5 rate and, in discharge, at a D/2.5 rate.
  • FIG. 7 represents the change in the capacity Q (in mAh/g) as a function of the current by weight. It is observed that the composite material according to the invention exhibits a good electrochemical performance.
  • Curve - ⁇ - sample according to the invention of example 6
  • Curve - ⁇ - sample according to the invention of example 7
  • a button cell is assembled in the following way, comprising:

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Nanotechnology (AREA)
  • Composite Materials (AREA)
  • Condensed Matter Physics & Semiconductors (AREA)
  • General Physics & Mathematics (AREA)
  • Physics & Mathematics (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Manufacturing & Machinery (AREA)
  • Battery Electrode And Active Subsutance (AREA)
US13/256,522 2009-03-19 2010-03-18 Fluorinated binder composite materials and carbon nanotubes for positive electrodes for lithium batteries Abandoned US20120028117A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
FR0901279 2009-03-19
FR0901279A FR2943463B1 (fr) 2009-03-19 2009-03-19 Materiaux composites a base de liants fluores et nanotubes de carbone pour electrodes positives de batteries lithium.
PCT/FR2010/050485 WO2010106292A1 (fr) 2009-03-19 2010-03-18 Materiaux composites a base de liants fluores et nanotubes de carbone pour electrodes positives de batteries lithium

Publications (1)

Publication Number Publication Date
US20120028117A1 true US20120028117A1 (en) 2012-02-02

Family

ID=41052359

Family Applications (1)

Application Number Title Priority Date Filing Date
US13/256,522 Abandoned US20120028117A1 (en) 2009-03-19 2010-03-18 Fluorinated binder composite materials and carbon nanotubes for positive electrodes for lithium batteries

Country Status (7)

Country Link
US (1) US20120028117A1 (ja)
EP (1) EP2409350A1 (ja)
JP (1) JP5684226B2 (ja)
KR (1) KR20110136867A (ja)
CN (1) CN102356490A (ja)
FR (1) FR2943463B1 (ja)
WO (1) WO2010106292A1 (ja)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20140346618A1 (en) * 2013-05-23 2014-11-27 Nexeon Limited Surface treated silicon containing active materials for electrochemical cells
US20150064559A1 (en) * 2012-03-30 2015-03-05 Sumitomo Osaka Cement Co., Ltd. Electrode-active material, lithium-ion battery, method for detecting discharge state of electrode-active material, and method for manufacturing electrode-active material
EP3203560A4 (en) * 2015-12-09 2017-11-08 LG Chem, Ltd. Lithium secondary battery positive electrode material slurry comprising at least two types of conductive materials, and lithium secondary battery using same
CN110168784A (zh) * 2017-05-12 2019-08-23 株式会社Lg化学 制造锂二次电池的方法
US10615405B2 (en) 2015-03-03 2020-04-07 Arkema France Electrodes of li-ion batteries with improved conductivity
US11038175B2 (en) 2017-03-22 2021-06-15 Lg Chem, Ltd. Positive electrode active material pre-dispersion composition including hydrogenated nitrile butadiene rubber as dispersant, positive electrode for secondary battery, and lithium secondary battery including the positive electrode
US11108050B2 (en) 2016-03-24 2021-08-31 Lg Chem, Ltd. Conductive material dispersed liquid and secondary battery manufactured using the same
FR3116158A1 (fr) * 2020-11-10 2022-05-13 Arkema France Procédé de synthèse de compositions phosphate de Fer Lithié - Carbone
US11367862B2 (en) 2018-08-28 2022-06-21 Samsung Electronics Co., Ltd. Cathode and lithium battery including the same

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6002577B2 (ja) 2009-05-29 2016-10-05 アーケマ・インコーポレイテッド 水性ポリフッ化ビニリデン組成物
US20120015246A1 (en) 2010-05-27 2012-01-19 Arkema Inc. Waterborne fluoropolymer composition
JP5720411B2 (ja) * 2011-05-11 2015-05-20 トヨタ自動車株式会社 非水電解質二次電池の製造方法
US9065136B2 (en) * 2011-09-14 2015-06-23 Samsung Sdi Co., Ltd. Positive electrode for rechargeable lithium battery, method of preparing the same, and rechargeable lithium battery including the same
US9985292B2 (en) * 2012-11-27 2018-05-29 Seeo, Inc. Oxyphosphorus-containing polymers as binders for battery cathodes
CN103000903B (zh) * 2012-11-28 2015-01-28 哈尔滨工业大学 一种掺杂碳纳米材料的前驱体及制备方法和球形锂金属氧化物正极材料及制备方法
KR101665656B1 (ko) * 2015-04-28 2016-10-12 충남대학교산학협력단 이차전지용 양극 및 이로부터 제조된 리튬이차전지
JP6737090B2 (ja) * 2016-09-09 2020-08-05 日産自動車株式会社 電気デバイス用正極及びそれを用いたリチウムイオン電池
FR3094371A1 (fr) * 2019-03-29 2020-10-02 Arkema France Formulation d’électrode pour BATTERIE LI-ION et procede de fabrication d’electrode par extrusion à faible temps de séjour
CN113036141A (zh) * 2021-03-10 2021-06-25 哈尔滨万鑫石墨谷科技有限公司 一种磷酸铁锂正极浆料的制备方法
FR3131094A1 (fr) * 2021-12-17 2023-06-23 Arkema France Composition de cathode pour batterie li-ion

Family Cites Families (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2513418B2 (ja) * 1993-06-24 1996-07-03 日本電気株式会社 電池電極合剤および非水電解液電池
JP2002246029A (ja) * 2001-02-20 2002-08-30 Atofina Japan Kk 結着剤組成物
JP4029315B2 (ja) * 2001-09-18 2008-01-09 株式会社デンソー リチウム二次電池用正極及びリチウム二次電池
JP2003331838A (ja) * 2002-05-14 2003-11-21 Hitachi Ltd リチウム二次電池
KR100484642B1 (ko) * 2002-09-23 2005-04-20 삼성에스디아이 주식회사 리튬-설퍼 전지용 양극 활물질 및 그 제조방법
US20040160156A1 (en) * 2003-02-19 2004-08-19 Matsushita Electric Industrial Co., Ltd. Electrode for a battery and production method thereof
CA2506104A1 (en) * 2005-05-06 2006-11-06 Michel Gauthier Surface modified redox compounds and composite electrode obtain from them
KR100796687B1 (ko) * 2005-11-30 2008-01-21 삼성에스디아이 주식회사 리튬 이차 전지용 활물질, 이의 제조방법 및 이를 포함하는 리튬 이차 전지
CN101479866B (zh) * 2006-06-27 2011-11-30 花王株式会社 锂电池正极用复合材料的制造方法
CN101087017A (zh) * 2006-09-08 2007-12-12 长沙理工大学 高功率大容量锂离子电池正极极片及其制作方法
CN101192682A (zh) * 2006-11-21 2008-06-04 比亚迪股份有限公司 一种锂离子二次电池及其制备方法
US20100028773A1 (en) * 2007-03-05 2010-02-04 Toyo Ink Mfg. Co., Ltd. Composition for battery
JP5139717B2 (ja) * 2007-05-18 2013-02-06 帝人株式会社 多層カーボンナノチューブ分散液およびその製造方法
JP2008300189A (ja) * 2007-05-31 2008-12-11 Fuji Heavy Ind Ltd 電極用構成材、それを用いた電極、およびリチウムイオン二次電池
JP5352069B2 (ja) * 2007-08-08 2013-11-27 トヨタ自動車株式会社 正極材料、正極板、二次電池、及び正極材料の製造方法
CN101090154A (zh) * 2007-08-14 2007-12-19 深圳市海盈科技有限公司 锂离子电池的正极组成物
JP5205863B2 (ja) * 2007-08-16 2013-06-05 ソニー株式会社 非水電解液二次電池
CN101281987A (zh) * 2008-05-22 2008-10-08 上海南都能源科技有限公司 磷酸亚铁锂基聚合物锂离子电池及其制造方法
CN101335347B (zh) * 2008-08-01 2010-06-02 黄德欢 锂离子电池的高导电性磷酸铁锂正极材料的制备方法

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20150064559A1 (en) * 2012-03-30 2015-03-05 Sumitomo Osaka Cement Co., Ltd. Electrode-active material, lithium-ion battery, method for detecting discharge state of electrode-active material, and method for manufacturing electrode-active material
US20150125595A1 (en) * 2013-05-23 2015-05-07 Nexeon Limited Surface treated silicon containing active materials for electrochemical cells
US9276261B2 (en) * 2013-05-23 2016-03-01 Nexeon Limited Surface treated silicon containing active materials for electrochemical cells
US9401506B2 (en) 2013-05-23 2016-07-26 Nexeon Limited Surface treated silicon containing active materials for electrochemical cells
US20140346618A1 (en) * 2013-05-23 2014-11-27 Nexeon Limited Surface treated silicon containing active materials for electrochemical cells
US10615405B2 (en) 2015-03-03 2020-04-07 Arkema France Electrodes of li-ion batteries with improved conductivity
EP3203560A4 (en) * 2015-12-09 2017-11-08 LG Chem, Ltd. Lithium secondary battery positive electrode material slurry comprising at least two types of conductive materials, and lithium secondary battery using same
US10128508B2 (en) 2015-12-09 2018-11-13 Lg Chem, Ltd. Positive electrode material slurry for lithium secondary battery including at least two conductive materials and lithium secondary battery using the same
US11108050B2 (en) 2016-03-24 2021-08-31 Lg Chem, Ltd. Conductive material dispersed liquid and secondary battery manufactured using the same
US11038175B2 (en) 2017-03-22 2021-06-15 Lg Chem, Ltd. Positive electrode active material pre-dispersion composition including hydrogenated nitrile butadiene rubber as dispersant, positive electrode for secondary battery, and lithium secondary battery including the positive electrode
US20200075928A1 (en) * 2017-05-12 2020-03-05 Lg Chem, Ltd. Method for manufacturing lithium secondary battery
CN110168784A (zh) * 2017-05-12 2019-08-23 株式会社Lg化学 制造锂二次电池的方法
US11664485B2 (en) * 2017-05-12 2023-05-30 Lg Energy Solution, Ltd. Method for manufacturing lithium secondary battery
US11367862B2 (en) 2018-08-28 2022-06-21 Samsung Electronics Co., Ltd. Cathode and lithium battery including the same
FR3116158A1 (fr) * 2020-11-10 2022-05-13 Arkema France Procédé de synthèse de compositions phosphate de Fer Lithié - Carbone
WO2022101566A1 (fr) * 2020-11-10 2022-05-19 Arkema France Procédé de synthese de compositions phosphate de fer lithié - carbone

Also Published As

Publication number Publication date
CN102356490A (zh) 2012-02-15
EP2409350A1 (fr) 2012-01-25
JP2012521065A (ja) 2012-09-10
FR2943463B1 (fr) 2011-07-01
WO2010106292A1 (fr) 2010-09-23
FR2943463A1 (fr) 2010-09-24
JP5684226B2 (ja) 2015-03-11
KR20110136867A (ko) 2011-12-21

Similar Documents

Publication Publication Date Title
US20120028117A1 (en) Fluorinated binder composite materials and carbon nanotubes for positive electrodes for lithium batteries
EP2503626B1 (en) Positive-electrode material for a lithium ion secondary battery, and manufacturing method therefor
JP5255143B2 (ja) 正極材料、これを用いたリチウムイオン二次電池、及び正極材料の製造方法
JP5228576B2 (ja) リチウムイオン二次電池及び電気自動車用電源
US11201327B2 (en) Lithium ion secondary battery
EP2113957B1 (en) Positive electrode for lithium secondary cell and lithium secondary cell using the same
JP6616326B2 (ja) カソードスラリを製造する方法およびカソード
EP3117474B1 (en) Cathode for lithium batteries
KR20180087162A (ko) 고온 저장 특성이 향상된 리튬 이차전지의 제조 방법
US20110135982A1 (en) Negative electrode for non-aqueous electrolyte secondary battery and fabrication method thereof, and non-aqueous electrolyte secondary battery
US10249874B2 (en) Composite negative active material, negative electrode including composite negative active material, and lithium secondary battery including negative electrode
US20220285686A1 (en) Globular carbon-based anode active material, method for manufacturing same, and anode and lithium secondary battery comprising same
EP2985824B1 (en) Cathode material, cathode including the same, and lithium battery including the cathode
KR20150137888A (ko) 복합 양극 활물질, 그 제조방법 및 이를 포함하는 리튬 전지
KR101590678B1 (ko) 리튬 이차전지용 음극 활물질 및 이를 포함하는 리튬 이차전지
KR20160005555A (ko) 리튬전지
KR20160001651A (ko) 리튬 이차전지
KR20180138126A (ko) 리튬-황 전지
US20230387384A1 (en) Method for Manufacturing Positive Electrode for Lithium Secondary Battery and Positive Electrode for Lithium Secondary Battery Manufactured Thereby
KR20170099642A (ko) 리튬 이차 전지용 음극 및 이를 포함하는 리튬 이차 전지
JP7336466B2 (ja) 非水電解質二次電池用負極およびその電池
CN114447279A (zh) 含硅负极、电化学电池及其制造方法
WO2020137403A1 (ja) 二次電池電極用炭素材料分散液、二次電池電極用スラリー組成物、二次電池用電極および二次電池
KR20200095182A (ko) 리튬 이차전지의 음극 활물질층 형성용 조성물, 이를 포함하는 리튬 이차전지용 음극 및 리튬 이차전지
US20220344660A1 (en) Globular carbon-based anode active material, method for manufacturing same, and anode and lithium secondary battery comprising same

Legal Events

Date Code Title Description
AS Assignment

Owner name: CENTRE NATIONAL DE LA RECHERCHE SCIENTIFIQUE, FRAN

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:PLEE, DOMINIQUE;LESTRIEZ, BERNARD;DESAEVER, SABRINA;AND OTHERS;SIGNING DATES FROM 20110920 TO 20111007;REEL/FRAME:027047/0427

Owner name: ARKEMA FRANCE, FRANCE

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:PLEE, DOMINIQUE;LESTRIEZ, BERNARD;DESAEVER, SABRINA;AND OTHERS;SIGNING DATES FROM 20110920 TO 20111007;REEL/FRAME:027047/0427

STCB Information on status: application discontinuation

Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION